Tool and method for producing a 3D molded pulp product
The document relates to a tool for producing a 3D molded product from a pulp slurry, comprising a pair of molds having respective product faces, that are configured to face each other and to press a pulp layer therebetween, said product faces providing a 3D shape for molding the 3D molded product, said product faces presenting a respective outer product face edge, defining an outermost limit of a forming area of mold. At least one of the product faces, as seen from the product face edge and inwardly towards a center of gravity of the product face, presents an outer zone (Z1) having effectively no porosity, and an inner zone (Z4) having a porosity of 40-75%, wherein a first intermediate zone (Z2) is arranged between the outer zone (Z1) and the inner zone (Z4), and has a porosity that is greater than that of the outer zone (Z1) and less than that of the inner zone (Z4).
Latest Celwise AB Patents:
- Tool or tool part, system including such a tool or tool part, method of producing such a tool or tool part and method of molding a product from a pulp slurry
- Method of producing a pulp product
- Pick-up press device and method of producing a 3D-molded product from a pulp slurry
- Laminated structure and method of its production
- Method of making double-walled structure, and structure formed by the method
This application claims priority to International Application No. PCT/EP2020/050059, filed Jan. 3, 2020 and titled “TOOL AND METHOD FOR PRODUCING A 3D MOLDED PULP PRODUCT,” which in turn claims priority from a Swedish Patent Application having serial number 1950005-7, filed Jan. 3, 2019, titled “TOOL AND METHOD FOR PRODUCING A 3D MOLDED PULP PRODUCT,” both of which are incorporated herein by reference in their entireties.
TECHNICAL FIELDThe present disclosure relates to a tool and a method for producing a molded pulp product. The method is particularly suitable for 3D molding of products from a pulp slurry. Such products may include trays, cups, plates and various containers for packaging.
BACKGROUNDFrom WO2016101976A1 there is known a method of producing products from a pulp slurry by applying the slurry layer to a porous mold and removing water from the slurry by simultaneously heating and pressing the slurry layer while drawing a vacuum through a mold wall, the other side of which being in contact with the slurry layer.
As is disclosed in WO2016101976A1, the molding process may be performed in two or more successive pressing steps, which is advantageous as it shortens cycle time and thus increases the throughput of the production process, as compared to a process with a single pressing step.
The production of pulp products using a porous mold is associated with various challenges resulting from the behavior of the pulp when interacting with the porous mold.
One particular problem which is addressed herein is the formation of a “beard” on inside corners of a mold. Such a “beard” is a result of a buildup of excessive amount of pulp. Such a beard has a negative impact on subsequent forming steps as well as on the appearance of the final product.
There is a need to reduce such “beard formation”.
SUMMARYAn object of the present disclosure is to provide an improved tool and method of forming a 3D molded pulp product.
The invention is defined by the appended independent claims, with embodiments being set forth in the appended dependent claims, in the following description and in the attached drawings.
According to a first aspect, there is provided a tool for producing a 3D molded product from a pulp slurry, comprising a pair of molds having respective product faces, that are configured to face each other and to press a pulp layer therebetween, said product faces providing a 3D shape for molding the 3D molded product, said product faces presenting a respective outer product face edge, defining an outermost limit of a forming area of at least one of the molds, preferably both, wherein at least one of the product faces, as seen from the product face edge and inwardly towards a center of gravity of the product face, presents an outer zone having effectively no porosity, and an inner zone having a porosity of 40-75%, wherein a first intermediate zone is arranged between the outer zone and the inner zone, and has a porosity that is greater than that of the outer zone and less than that of the inner zone.
The term “porosity” is defined as the ratio of pore surface to total surface of a given area of a zone.
By gradually reducing the porosity at the brim area, the vacuum formed at the outermost portion of the mold is gradually reduced and thus buildup of an excessive amount of pulp at the outermost portion of the mold can be prevented or eliminated.
The outer zone can present a porosity of less than 1%, preferably less than 0.5% or less than 0.1%.
The first intermediate zone can present a porosity that is 25-75% of that of the inner zone.
The product face can present a second intermediate zone having a porosity that is greater than that of the first intermediate zone but less than that of the inner zone.
The second intermediate zone can present a porosity that is 40-85% of that of the inner zone.
The porous product face can present pores having a greatest cross sectional width of 0.1-0.7 mm, preferably 0.25-0.6 mm.
The first intermediate zone can present pores having a smaller average greatest cross section than the pores presented by the inner zone.
The second intermediate zone can present pores having a greater average greatest cross section than the pores presented by the first intermediate zone.
The mold can comprise a brim portion which runs around a periphery of the mold and which presents an angle of more than 60 degrees, preferably more than 75 degrees or 85-90 degrees to a relative movement direction of the molds.
The outer zone can be formed in the brim portion.
The outer zone can be outwardly limited by a wall which extends at an angle of less than 50 degrees, preferably less than 30 degrees or 0-10 degrees to the relative movement direction of the molds.
The outer zone can extend inwardly from an imaginary point of intersection between the wall and the brim portion by a distance of less than 0.5 mm, preferably less than 0.3 mm.
Thus, a soft transition may be present between the wall and the brim portion of the mold.
The “imaginary point of intersection” is defined as a point where an imaginary line along the wall intersects an imaginary line along the brim portion, as seen in a cross-sectional plane perpendicular to the wall and the brim portion.
According to a second aspect of the present disclosure, a method of producing a 3D molded product from a pulp slurry is provided, the method comprising applying a pulp slurry layer to a porous product face of a first mold; in a first forming step, pressing the pulp slurry layer against the porous product face of the first mold, while heating the pulp slurry layer and drawing a vacuum through the porous forming face of the first mold, wherein the vacuum drawn through the porous forming face of the first mold is gradually reduced towards an outer product face edge, which defines an outermost limit of a forming area of the tool, said reduction being achieved through gradual reduction of a porosity of the porous forming face.
The first mold may form part of a mold set according to what has been described above.
The method may further comprise transferring the pulp slurry layer to a porous forming face of a second mold, and in a second, subsequent, forming step, pressing the pulp slurry layer against the porous forming face of the second mold, while heating the pulp slurry layer and drawing a vacuum through the porous forming face of the second mold.
In the first forming step, the forming face of the first mold can be heated to about 150-400° C., preferably 200-300° C.
In the first forming step, the pulp slurry layer can be pressed against the forming face of the first mold with a pressure of about 390-1570 kPa, preferably 580-1170 kPa.
In the first forming step, the pulp slurry layer can be pressed against the forming face of the first mold during a first pressing time of 0.1-4.0 second, preferably 0.5-2.0 second.
In the first forming step, an initial water content of the pulp slurry layer can be 70-90% by weight and a final water content can be 45-65% by weight, preferably about 50-60% by weight.
A vacuum level at the rear side of the forming face of the second mold can be 50-99 kPa, preferably 65-85 kPa.
The method can further comprise transferring the pulp slurry layer to a porous forming face of a third mold, and in a third, subsequent, forming step, pressing the pulp slurry layer against the porous forming face of the third mold, while heating the pulp slurry layer and drawing a vacuum through the porous forming face of the third mold, wherein a vacuum level in the second forming step is greater than in the third forming step.
A third vacuum level at the rear side of the forming face of the third mold can be 50-99 kPa, preferably 65-85 kPa.
In the third forming step, the forming face of the third mold can be heated to about 100-300° C., preferably 200-280° C.
In the third forming step, the pulp slurry layer can be pressed against the forming face of the third mold with a pressure of about 390-1570 kPa, preferably 580-1170 kPa.
In the third forming step, the pulp slurry layer can be pressed against the forming face of the third mold during a third pressing time of 0.1-4.0 second, preferably 0.5-2.0 second.
In the third forming step, an initial water content of the pulp slurry layer can be about 25-45% or 25-40% by weight, preferably about 30-40% or 30-35% by weight, and a final water content can be less than about 5% by weight, preferably less than about 1% by weight.
The first mold can be a pick-up mold, on which pulp slurry is applied from liquid form, said pulp slurry having a pulp concentration of less than 0.5% by weight, preferably less than 0.49% or 0.005-0.025%.
While the pickup tool is immersed in the pulp slurry 2, the pressure regulator P1 may generate a vacuum, causing pulp fibers 3 to stick to a product face of the pickup tool 10.
During the transfer of the pulp fibers 3 from the pickup tool to the transfer tool, an air pressure greater than ambient pressure may be generated by the first pressure regulator P1 to cause the pulp fibers to release from the pickup tool.
Alternatively, or as a supplement, a vacuum may be generated by the second pressure regulator P2, causing the pulp fibers to be received by the transfer tool 20.
One, or both, of the pressing tools may be provided with a heating element 33, 43, energized by an energy supply E1, E2 and optionally controlled by a controller C. The heating may be achieved by electric heating elements, hot air or liquid or induction.
The pressing tools and their associated tool holders may be movable relative one another between an open position, wherein a partially molded pulp product may be inserted, and a pressing position, wherein the pressing tools are forced towards each other thus pressing the product 3″ between product faces of the respective tool 30, 40.
When in the pressing position, heat may be supplied by one, or both, of the heaters 33, 43.
During the pressing step, one or both pressure regulators P3, P4 may provide a vacuum to assist in the evacuation of water vapor from the product 3″.
As an alternative, one of the pressure regulators may provide a vacuum while the other one provides a pressure greater than the ambient air pressure.
Optionally, hot air or steam may be introduced through the molds during the pressing process (
It is noted that two or more successive pressing steps may be used, e.g. to gradually form all or parts of the product 3″ and/or to apply additional features to the product, such as coatings, decors and the like.
In one embodiment, steps are performed in accordance with what has been described with respect to
Referring to
In a first step 101, a pulp slurry layer is provided, e.g. as described with reference to
Alternatively, the pulp slurry may be applied to the pickup tool by a coating operation, such as spray coating.
In a second step 102, the pulp slurry layer is transferred from the pickup tool to a first press tool. The transfer may be performed by the pickup tool, or by means of a separate transfer tool, which may have a transfer tool wall portion that is porous. During the transfer step, a vacuum may be applied to the rear side of the transferring tool wall, such that the pulp slurry layer is held to the transferring tool wall. In order to release the pulp slurry layer from the transferring tool wall, it is possible to instead apply pressurized air to the rear side of the transferring tool wall.
Alternatively, the pulp slurry layer may be applied directly to the first press tool. That is, the pulp slurry layer may be formed directly on the first press tool by application of the pulp slurry to the porous forming face of the first press tool. The pulp slurry layer may be applied directly to the first press tool by submerging a tool part of the first press tool, presenting a porous wall portion, in a pulp slurry with vacuum being applied to a rear side of the porous wall portion. Alternatively, the pulp slurry may be applied to the porous forming face of the first press tool by a coating operation, such as spray coating.
In a third step 103, the pulp slurry layer may be pressed in the first press tool, which may comprise a pair of mating tool parts, one of which may have a porous wall portion, which contacts the pulp slurry layer, and through which a vacuum can be drawn.
In this first pressing step 103, a pressure lower than the surrounding ambient pressure is applied at a rear side of the porous wall portion, thus resulting in a vacuum at the rear side of the porous wall portion, causing solvent vapor, such as steam, to be drawn through the tool.
The pressure applied to the rear side of the porous wall portion may be on the order of low or medium level vacuum. That is, the pressure may be more than 1 Pa, but less than ambient pressure. Preferably, the pressure may be on the order of 1 kPa to ambient pressure.
In the first pressing step, a first vacuum level at the rear side of the forming face of the first mold may be about 50-99 kPa, and typically 65-85 kPa.
In the first pressing step, a first pressure at a rear side of the forming face of the first mold may be 200-900 mbarA (millibar absolute), preferably 300-800 mbarA.
The forming face of the first mold may be heated to about 150-500° C., preferably 150-400° C., 200-500° C., 200-400° C., or 200-300° C., and in most cases 240-280° C. Typically, all mold faces contacting the pulp slurry are heated.
A pressing pressure between mold faces may be on the order of about 390-1570 kPa, and in most cases 580-1170 kPa.
The pressing pressure may be applied during a first pressing time of 0.1-4.0 second, preferably 0.5-2.0 second. In most settings, a pressing time on the order of 0.5-1.5 second is sufficient, and often also 0.5-1 second.
Typically, in this first step, an initial water content of the pulp slurry layer is 70-90% by weight and after the pressing step has been performed, a final water content may be 45-65% by weight, typically about 50-60% by weight.
After the first pressing step 103, the pulp slurry layer, now with a substantial amount of its solvent removed, may be transferred 104 to a second press tool. The transfer 104 may be performed in the same manner as the first transfer step 102, and with similar equipment. The second press tool may be designed essentially as the first press tool.
In a second pressing step 105, the pulp slurry layer may be pressed in the second press tool, which may comprise a pair of mating tool parts, one of which may have a porous wall portion, which contacts the pulp slurry layer, and through which a vacuum can be drawn.
In this second pressing step 105, a pressure lower than the surrounding ambient pressure is applied at a rear side of the porous wall portion, thus resulting in a vacuum at the rear side of the porous wall portion, causing solvent vapor, such as steam, to be drawn through the tool.
In the second pressing step, a second vacuum level at the rear side of the forming face of the second mold may be about 50-99 kPa, and typically 65-85 kPa, but always lower vacuum level than in the first pressing step.
In the second pressing step, a second pressure at a rear side of the forming face of the second mold may be 200-900 mbarA (millibar absolute), preferably 300-800 mbarA.
The forming face of the second mold may be heated to about 110-500° C., preferably 110-400° C., 150-500° C., 150-400° C., 200-500° C., 200-400° C., or 200-300° C., and in most cases 240-280° C. Typically, all mold faces making up the second mold and contacting the pulp slurry layer may be heated.
A pressing pressure between mold faces may be on the order of about 390-1570 kPa, and in most cases 580-1170 kPa.
The pressing pressure may be applied during a second pressing time of 0.1-4.0 second, preferably 0.5-2.0 second. In most settings, a pressing time on the order of 0.5-1.5 second is sufficient, and often also 0.5-1 second.
Typically, in this second pressing step, an initial water content of the pulp slurry layer may be about 45-65%, typically about 50-60% by weight.
A final water content may be about 25-40% by weight, preferably about 30-35% by weight.
After the second pressing step 105, the pulp slurry layer, now with a substantial amount of its solvent removed, may be transferred 106 to a third press tool. The transfer 106 may be performed in the same manner as the first transfer step 102 and/or the second transfer step 104, and with similar equipment. The third press tool may be designed essentially as the first press tool.
In a third pressing step 107, the pulp slurry layer may be pressed in the third press tool, which may comprise a pair of mating tool parts, one of which may have a porous wall portion, which contacts the pulp slurry layer, and through which a vacuum can be drawn.
In this third pressing step 107, a pressure lower than the surrounding ambient pressure is applied at a rear side of the porous wall portion, thus resulting in a vacuum at the rear side of the porous wall portion, causing solvent vapor, such as steam, to be drawn through the tool.
In the third pressing step, a third vacuum level at the rear side of the forming face of the third mold may be about 50-99 kPa, and typically 65-85 kPa, but always lower vacuum level than in the second pressing step.
In the third pressing step, a third pressure at a rear side of the forming face of the third mold may be 200-900 mbarA (millibar absolute), preferably 300-800 mbarA.
The forming face of the third mold may be heated to about 100-400° C., preferably 100-300° C., 150-400° C., 150-300° C., 200-300° C., or 200-280° C., and in most cases 240-280° C. Typically, all mold faces making up the third mold and contacting the pulp slurry layer may be heated.
A pressing pressure between mold faces may be on the order of about 390-1570 kPa, and in most cases 580-1170 kPa.
The pressing pressure may be applied during a third pressing time of 0.1-4.0 second, preferably 0.5-2.0 second. In most settings, a pressing time on the order of 0.5-1.5 second is sufficient, and often also 0.5-1 second.
Typically, in this third pressing step, an initial water content of the pulp slurry layer may be about 25-45% or 25-40% by weight, preferably about 30-40% or 30-35% by weight, and a final water content may be less than about 5% by weight, preferably less than about 1% by weight.
After the third pressing step 107, the pulp slurry layer, now with most of its solvent removed, may be transferred 108 out of the machine.
Optionally, additional steps, such as surface treatment, cutting or printing may be performed on the thus essentially dry product. The product may then be packaged, stored and shipped.
It is noted that the third pressing step 107, and thus also its related transfer step 106, is optional. Hence, the process may be finished after the second pressing step 105 with the output step 108 following immediately.
Thus, in the first pressing step, an initial water content of the pulp slurry layer may be 70-90% by weight and a final water content may be 25-50% by weight, preferably about 30-35% by weight.
In the second pressing step, an initial water content of the pulp slurry layer may be about 25-50%, preferably about 30-35% by weight, and a final water content may be less than about 5% by weight, preferably less than about 1% by weight.
Referring to
The brim 302, 402 may be substantially planar and may surround the out-of-plane portion 301, 401.
While the brim portion may be substantially planar and extend substantially perpendicular to a relative movement direction of the molds during the final part of the pressing operation, the brim wall 303, 403 may extend substantially perpendicularly to the brim portion 302, 402.
In reality, the brim portion 302, 402 may extend 60-90 degrees relative to the movement direction, preferably 75-90 degrees, 85-90 degrees or 89-90 degrees.
Likewise, the wall portion 303, 403 may extend 0-60 degrees relative to the movement direction, preferably 0-45 degrees, 0-30 degrees, 0-15 degrees, 0-5 degrees or 0-1 degrees.
The brim portion may extend from an imaginary point of intersection between the surface of the wall portion 303, 403 and the surface of the brim portion 302, 402. Thus, for each mold, a soft transition may be present between the wall 303, 403 and the brim portion 302, 402 respectively, wherein the “imaginary point of intersection” is the point where an imaginary line along the wall intersects an imaginary line along the brim portion, as seen in a cross-sectional plane perpendicular to the wall and the brim portion.
The extent of the brim portion may be a total of 1-15 mm, wherein each zone extends over less than 1 mm, preferably less than 0.5 mm or less than 0.3 mm.
As mentioned above, one or both of the molds 30, 40 may have a porous forming face. In the illustrated example, the female mold 40 is illustrated as having the porous forming face, but it may also, or instead, be the male mold 30 that has the porous forming face.
At a central portion of the mold 30, 40, there may be a predetermined nominal porosity, which may be constant or which may vary over the central portion.
The central portion may be anything inside the brim portion and any transition from the brim portion to the wall.
At the brim portion 402, there may be a gradually reducing porosity, with zero porosity at the outermost part of the brim portion 402.
In the illustrated example, the brim portion 402 is divided into three zones: a first zone Z1 with zero or very low porosity; a second zone Z2 with greater porosity, a third zone Z3, which is optional, and having even greater porosity than the second zone Z2 and then the inner zone Z4 having the nominal porosity.
Claims
1. A tool for producing a 3D molded product from a pulp slurry, comprising:
- a pair of molds having respective product faces, that are configured to face each other and to press a pulp slurry layer therebetween,
- said product faces providing a 3D shape for molding the 3D molded product,
- said product faces presenting a respective outer product face edge, defining an outermost limit of a forming area of at least one of the molds,
- wherein at least one of the product faces, as seen from the product face edge and inwardly towards a center of gravity of the product face, presents:
- an outer zone having effectively no porosity such that the outer zone presents a porosity of less than 1%,
- an inner zone having a porosity of 40-75%, and
- a first intermediate zone, arranged between the outer zone and the inner zone, and having a porosity that is greater than that of the outer zone and less than that of the inner zone.
2. The tool as claimed in claim 1, wherein the outer zone presents a porosity of less than 0.5%.
3. The tool as claimed in claim 1, wherein the first intermediate zone presents a porosity that is 25-75% of that of the inner zone.
4. The tool as claimed in claim 1, wherein the product face presents a second intermediate zone having a porosity that is greater than that of the first intermediate zone but less than that of the inner zone.
5. The tool as claimed in claim 4, wherein the second intermediate zone presents a porosity that is 40-85% of that of the inner zone.
6. The tool as claimed in claim 1, wherein the porous product face presents pores having a greatest cross sectional width of 0.1-0.7 mm.
7. The tool as claimed in claim 6, wherein the first intermediate zone presents pores having a smaller average greatest cross section than the pores presented by the inner zone.
8. The tool as claimed in claim 7, wherein the second intermediate zone presents pores having a greater average greatest cross section than the pores presented by the first intermediate zone.
9. The tool as claimed in claim 1, wherein the mold comprises a brim portion which runs around a periphery of the mold and which presents an angle of more than 60 degrees to a relative movement direction of the molds.
10. The tool as claimed in claim 9, wherein the outer zone is formed in the brim portion.
11. The tool as claimed in claim 9, wherein the outer zone is outwardly limited by a wall which extends at an angle of less than 50 degrees to the relative movement direction of the molds.
12. The tool as claimed in claim 11, wherein the outer zone extends inwardly from an imaginary point of intersection between the wall and the brim portion by a distance of less than 0.5 mm.
13. A method of producing a 3D molded product from a pulp slurry, comprising:
- providing a tool according to claim 1,
- applying a pulp slurry layer to a porous product face of a first mold of said tool,
- in at least one forming step, pressing the pulp slurry layer to form said 3D molded product.
14. The method according to claim 13, comprising: in a first forming step, pressing the pulp slurry layer against the porous product face of the first mold.
15. The method according to claim 14, wherein the pressing is performed while drawing a vacuum through the porous product face of the first mold,
- wherein the vacuum drawn through the porous product face of the first mold is gradually reduced towards the outer product face edge, which defines an outermost limit of a forming area of the first mold,
- said reduction being achieved through gradual reduction of a porosity of the porous product face of the first mold.
16. The method according to claim 14, wherein the pressing is performed while heating the pulp slurry layer.
17. The method according to claim 14, wherein, in the first forming step, an initial water content of the pulp slurry layer is 70-90% by weight.
18. A tool for producing a 3D molded product from a pulp slurry comprising at least a first mold,
- the first mold having a porous product face providing a 3D shape for molding the 3D molded product,
- said porous product face presenting an outer product face edge, defining an outermost limit of a forming area of the first mold,
- wherein the first mold presents a gradual reduction of a porosity of the porous product face from an inner part of the product face to the outer product face edge.
19. The tool according to claim 18, wherein the product face, as seen from the product face edge and inwardly towards a center of gravity of the product face, presents:
- an outer zone having effectively no porosity such that the outer zone presents a porosity of less than 1%,
- an inner zone having a porosity of 40-75%, and
- a first intermediate zone, arranged between the outer zone and the inner zone, and having a porosity that is greater than that of the outer zone and less than that of the inner zone.
20. The tool according to claim 18, further comprising a second mating mold, wherein the first mold and the second mating mold forms a pair of molds having respective product faces, that are configured to face each other and to press a pulp slurry layer therebetween.
21. A method of producing a 3D molded product from a pulp slurry, comprising:
- providing a tool according to claim 20,
- applying a pulp slurry layer to a porous product face of a first mold of said tool,
- in at least one forming step, pressing the pulp slurry layer to form said 3D molded product.
| 1709338 | April 1929 | Chaplin |
| 1793089 | February 1931 | Heyes |
| 2377864 | June 1945 | Chaplin |
| 2927635 | March 1960 | Crane |
| 2990314 | June 1961 | Leitzel |
| 3067470 | December 1962 | Stickney et al. |
| 3075872 | January 1963 | Reifers |
| 3161705 | December 1964 | Kindseth |
| 3261740 | July 1966 | Wells |
| 3284284 | November 1966 | Wells |
| 3325349 | June 1967 | Reifers |
| 3793138 | February 1974 | Rohrer |
| 4014737 | March 29, 1977 | Brennan |
| 4337116 | June 29, 1982 | Foster et al. |
| 5039465 | August 13, 1991 | Freeman et al. |
| 5356518 | October 18, 1994 | Kelley et al. |
| 5399243 | March 21, 1995 | Miyamoto et al. |
| 5431784 | July 11, 1995 | Miyamoto et al. |
| 5547544 | August 20, 1996 | Miyamoto et al. |
| 5603808 | February 18, 1997 | Nishikawa |
| 5685956 | November 11, 1997 | Greve |
| 5745971 | May 5, 1998 | Ohsawa et al. |
| 5795443 | August 18, 1998 | Greve |
| 6210531 | April 3, 2001 | Bradford |
| 6461480 | October 8, 2002 | Otakura et al. |
| 6468398 | October 22, 2002 | Kumamoto et al. |
| 6576089 | June 10, 2003 | Sato et al. |
| 6605187 | August 12, 2003 | Nonomura et al. |
| 6645348 | November 11, 2003 | Kumamoto et al. |
| 6752910 | June 22, 2004 | Sato et al. |
| 9149948 | October 6, 2015 | Kuo et al. |
| 9650746 | May 16, 2017 | Choda et al. |
| 9739016 | August 22, 2017 | Kuo et al. |
| 9803322 | October 31, 2017 | Kuo et al. |
| 9856608 | January 2, 2018 | Chung et al. |
| 10435848 | October 8, 2019 | Andersson |
| 10801164 | October 13, 2020 | Andersson |
| 11391001 | July 19, 2022 | Andersson |
| 20030111201 | June 19, 2003 | Sato et al. |
| 20050230863 | October 20, 2005 | Scott et al. |
| 20070164041 | July 19, 2007 | Pierce et al. |
| 20090139678 | June 4, 2009 | Nilsson |
| 20090142523 | June 4, 2009 | Nilsson et al. |
| 20090283526 | November 19, 2009 | Pierce et al. |
| 20090291531 | November 26, 2009 | Sato |
| 20100279007 | November 4, 2010 | Briselden et al. |
| 20100291401 | November 18, 2010 | Medina et al. |
| 20110172798 | July 14, 2011 | Staiger et al. |
| 20160145811 | May 26, 2016 | Socci et al. |
| 20160168793 | June 16, 2016 | Kuo et al. |
| 20160168800 | June 16, 2016 | Kuo et al. |
| 20160168801 | June 16, 2016 | Kuo et al. |
| 20160244917 | August 25, 2016 | Kuo et al. |
| 20160368235 | December 22, 2016 | Kuo et al. |
| 20170226699 | August 10, 2017 | Halvardsson et al. |
| 20170284206 | October 5, 2017 | Roberts et al. |
| 20170370049 | December 28, 2017 | Andersson et al. |
| 20180187379 | July 5, 2018 | Sundblad et al. |
| 20190169800 | June 6, 2019 | Hardacre et al. |
| 20190194870 | June 27, 2019 | Kuo et al. |
| 20190284764 | September 19, 2019 | Kuo et al. |
| 20190301102 | October 3, 2019 | Kuo et al. |
| 20190376238 | December 12, 2019 | Andersson et al. |
| 20190376239 | December 12, 2019 | Andersson et al. |
| 20210269983 | September 2, 2021 | Pierce |
| 20210316935 | October 14, 2021 | Pierce |
| 20220049432 | February 17, 2022 | Pierce |
| 20220403604 | December 22, 2022 | Andersson et al. |
| 20230107827 | April 6, 2023 | Briden |
| 20230340733 | October 26, 2023 | Turner |
| 20230364831 | November 16, 2023 | Goldberg |
| 20230392322 | December 7, 2023 | Pierce |
| 343455 | May 1978 | AT |
| 1046952 | November 1990 | CN |
| 1099830 | March 1995 | CN |
| 103751852 | April 2014 | CN |
| 204849488 | December 2015 | CN |
| 205443807 | August 2016 | CN |
| 205688279 | November 2016 | CN |
| 309870 | December 2003 | CZ |
| 102017219812 | May 2019 | DE |
| 102018003447 | October 2019 | DE |
| 0466653 | January 1992 | EP |
| 0559490 | September 1993 | EP |
| 0559491 | September 1993 | EP |
| 0728868 | August 1996 | EP |
| 3985170 | April 2022 | EP |
| 2927756 | November 2022 | ES |
| 1284406 | February 1962 | FR |
| 468622 | July 1937 | GB |
| 1411438 | October 1975 | GB |
| 2456502 | July 2009 | GB |
| S51131942 | October 1976 | JP |
| S63282301 | November 1988 | JP |
| H06128900 | May 1994 | JP |
| H06316900 | November 1994 | JP |
| H0724855 | January 1995 | JP |
| H0742100 | February 1995 | JP |
| H08197553 | August 1996 | JP |
| H08260400 | October 1996 | JP |
| H09195200 | July 1997 | JP |
| H09300446 | November 1997 | JP |
| H09309153 | December 1997 | JP |
| H09324399 | December 1997 | JP |
| 2000054298 | February 2000 | JP |
| 2001140200 | May 2001 | JP |
| 2002201600 | July 2002 | JP |
| 2003138500 | May 2003 | JP |
| 2003306898 | October 2003 | JP |
| 2007126757 | May 2007 | JP |
| 2009293157 | December 2009 | JP |
| 2013129921 | July 2013 | JP |
| 2015086478 | May 2015 | JP |
| 3221127 | May 2019 | JP |
| 2022515888 | February 2022 | JP |
| 20190000074 | January 2019 | KR |
| M511949 | November 2015 | TW |
| M515462 | January 2016 | TW |
| M515566 | January 2016 | TW |
| M519157 | March 2016 | TW |
| 201711926 | April 2017 | TW |
| 621751 | April 2018 | TW |
| 9722755 | June 1997 | WO |
| 98035097 | August 1998 | WO |
| 0058556 | October 2000 | WO |
| 0116428 | March 2001 | WO |
| 03035980 | May 2003 | WO |
| 2006057610 | June 2006 | WO |
| 2006057611 | June 2006 | WO |
| WO-2006057609 | June 2006 | WO |
| 2007084067 | July 2007 | WO |
| 2007106026 | September 2007 | WO |
| 2007129972 | November 2007 | WO |
| 2009132318 | October 2009 | WO |
| 2010124300 | October 2010 | WO |
| 2011059391 | May 2011 | WO |
| 2011059392 | May 2011 | WO |
| 2011059393 | May 2011 | WO |
| 2011059394 | May 2011 | WO |
| 2011065911 | June 2011 | WO |
| WO11135512 | November 2011 | WO |
| 2011159240 | December 2011 | WO |
| 2012005683 | January 2012 | WO |
| 2012033449 | March 2012 | WO |
| 2014051447 | April 2014 | WO |
| WO14105456 | July 2014 | WO |
| WO14110679 | July 2014 | WO |
| WO14150503 | September 2014 | WO |
| 2016055073 | April 2016 | WO |
| 2016101976 | June 2016 | WO |
| 2018199993 | November 2018 | WO |
| 2018237279 | December 2018 | WO |
| 2019066659 | April 2019 | WO |
| 2020016407 | January 2020 | WO |
| 2020016409 | January 2020 | WO |
| 2020016411 | January 2020 | WO |
| 2020016413 | January 2020 | WO |
| 2020016416 | January 2020 | WO |
| WO-2020141208 | July 2020 | WO |
- Swedish First Office Action and Search Report for Swedish Application No. 1950005-7, mailed Jun. 25, 2019, (6 pages).
- International Preliminary Report on Patentability for International Application No. PCT/EP2020/050059, mailed Jul. 15, 2021, (7 pages).
- Japanese Notice of Reasons for Refusal, and English Translation therefore, for Japanese Application No. 2021-538392, mailed Nov. 28, 2023, (10pages).
- International Search Report and Written Opinion for International Application No. PCT/EP2020/050059, mailed Feb. 17, 2020, (12 pages).
- Japanese Decision of Refusal, and English Translation therefore, for Japanese Counterpart Application No. 2021-538392, mailed Sep. 3, 2024, (12 pages).
Type: Grant
Filed: Jan 3, 2020
Date of Patent: May 13, 2025
Patent Publication Number: 20220049432
Assignee: Celwise AB (Norrköping)
Inventor: David Pierce (Norrköping)
Primary Examiner: Jose A Fortuna
Application Number: 17/419,890
International Classification: D21J 3/10 (20060101); B29C 33/02 (20060101); B29C 33/38 (20060101);
